Oscillatory Rheology Measuring the Viscoelastic Behaviour of Soft Materials
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Fluid Inertia and End Effects in Rheometer Flows
FLUID INERTIA AND END EFFECTS IN RHEOMETER FLOWS by JASON PETER HUGHES B.Sc. (Hons) A thesis submitted to the University of Plymouth in partial fulfilment for the degree of DOCTOR OF PHILOSOPHY School of Mathematics and Statistics Faculty of Technology University of Plymouth April 1998 REFERENCE ONLY ItorriNe. 9oo365d39i Data 2 h SEP 1998 Class No.- Corrtl.No. 90 0365439 1 ACKNOWLEDGEMENTS I would like to thank my supervisors Dr. J.M. Davies, Prof. T.E.R. Jones and Dr. K. Golden for their continued support and guidance throughout the course of my studies. I also gratefully acknowledge the receipt of a H.E.F.C.E research studentship during the period of my research. AUTHORS DECLARATION At no time during the registration for the degree of Doctor of Philosophy has the author been registered for any other University award. This study was financed with the aid of a H.E.F.C.E studentship and carried out in collaboration with T.A. Instruments Ltd. Publications: 1. J.P. Hughes, T.E.R Jones, J.M. Davies, *End effects in concentric cylinder rheometry', Proc. 12"^ Int. Congress on Rheology, (1996) 391. 2. J.P. Hughes, J.M. Davies, T.E.R. Jones, ^Concentric cylinder end effects and fluid inertia effects in controlled stress rheometry, Part I: Numerical simulation', accepted for publication in J.N.N.F.M. Signed ...^.^Ms>3.\^^. Date Ik.lp.^.m FLUH) INERTIA AND END EFFECTS IN RHEOMETER FLOWS Jason Peter Hughes Abstract This thesis is concerned with the characterisation of the flow behaviour of inelastic and viscoelastic fluids in steady shear and oscillatory shear flows on commercially available rheometers. -
On Exact Solution of Unsteady MHD Flow of a Viscous Fluid in An
Rana et al. Boundary Value Problems 2014, 2014:146 http://www.boundaryvalueproblems.com/content/2014/1/146 R E S E A R C H Open Access On exact solution of unsteady MHD flow of a viscous fluid in an orthogonal rheometer Muhammad Afzal Rana1, Sadia Siddiqa2* and Saima Noor3 *Correspondence: [email protected] Abstract 2Department of Mathematics, COMSATS Institute of Information This paper studies the unsteady MHD flow of a viscous fluid in which each point of Technology, Attock, Pakistan the parallel planes are subject to the non-torsional oscillations in their own planes. Full list of author information is The streamlines at any given time are concentric circles. Exact solutions are obtained available at the end of the article and the loci of the centres of these concentric circles are discussed. It is shown that the motion so obtained gives three infinite sets of exact solutions in the geometry of an orthogonal rheometer in which the above non-torsional oscillations are superposed on the disks. These solutions reduce to a single unique solution when symmetric solutions are looked for. Some interesting special cases are also obtained from these solutions. Keywords: viscous fluid; MHD flow; orthogonal rheometer; eccentric rotation; exact solutions 1 Introduction Berker [] has defined the ‘pseudo plane motions’ of the first kind that: if the streamlines in a plane flow are contained in parallel planes but the velocity components are dependent on the coordinate normal to the planes. Berker [] has obtained a class of exact solutions to the Navier-Stokes equations belonging to the above type of flows. -
Engineering Viscoelasticity
ENGINEERING VISCOELASTICITY David Roylance Department of Materials Science and Engineering Massachusetts Institute of Technology Cambridge, MA 02139 October 24, 2001 1 Introduction This document is intended to outline an important aspect of the mechanical response of polymers and polymer-matrix composites: the field of linear viscoelasticity. The topics included here are aimed at providing an instructional introduction to this large and elegant subject, and should not be taken as a thorough or comprehensive treatment. The references appearing either as footnotes to the text or listed separately at the end of the notes should be consulted for more thorough coverage. Viscoelastic response is often used as a probe in polymer science, since it is sensitive to the material’s chemistry and microstructure. The concepts and techniques presented here are important for this purpose, but the principal objective of this document is to demonstrate how linear viscoelasticity can be incorporated into the general theory of mechanics of materials, so that structures containing viscoelastic components can be designed and analyzed. While not all polymers are viscoelastic to any important practical extent, and even fewer are linearly viscoelastic1, this theory provides a usable engineering approximation for many applications in polymer and composites engineering. Even in instances requiring more elaborate treatments, the linear viscoelastic theory is a useful starting point. 2 Molecular Mechanisms When subjected to an applied stress, polymers may deform by either or both of two fundamen- tally different atomistic mechanisms. The lengths and angles of the chemical bonds connecting the atoms may distort, moving the atoms to new positions of greater internal energy. -
Lecture 1: Introduction
Lecture 1: Introduction E. J. Hinch Non-Newtonian fluids occur commonly in our world. These fluids, such as toothpaste, saliva, oils, mud and lava, exhibit a number of behaviors that are different from Newtonian fluids and have a number of additional material properties. In general, these differences arise because the fluid has a microstructure that influences the flow. In section 2, we will present a collection of some of the interesting phenomena arising from flow nonlinearities, the inhibition of stretching, elastic effects and normal stresses. In section 3 we will discuss a variety of devices for measuring material properties, a process known as rheometry. 1 Fluid Mechanical Preliminaries The equations of motion for an incompressible fluid of unit density are (for details and derivation see any text on fluid mechanics, e.g. [1]) @u + (u · r) u = r · S + F (1) @t r · u = 0 (2) where u is the velocity, S is the total stress tensor and F are the body forces. It is customary to divide the total stress into an isotropic part and a deviatoric part as in S = −pI + σ (3) where tr σ = 0. These equations are closed only if we can relate the deviatoric stress to the velocity field (the pressure field satisfies the incompressibility condition). It is common to look for local models where the stress depends only on the local gradients of the flow: σ = σ (E) where E is the rate of strain tensor 1 E = ru + ruT ; (4) 2 the symmetric part of the the velocity gradient tensor. The trace-free requirement on σ and the physical requirement of symmetry σ = σT means that there are only 5 independent components of the deviatoric stress: 3 shear stresses (the off-diagonal elements) and 2 normal stress differences (the diagonal elements constrained to sum to 0). -
Rheometry SLIT RHEOMETER
Rheometry SLIT RHEOMETER Figure 1: The Slit Rheometer. L > W h. ∆P Shear Stress σ(y) = y (8-30) L −∆P h Wall Shear Stress σ = −σ(y = h/2) = (8-31) w L 2 NEWTONIAN CASE 6Q Wall Shear Rateγ ˙ = −γ˙ (y = h/2) = (8-32) w h2w σ −∆P h3w Viscosity η = w = (8-33) γ˙ w L 12Q 1 Rheometry SLIT RHEOMETER NON-NEWTONIAN CASE Correction for the real wall shear rate is analogous to the Rabinowitch correction. 6Q 2 + β Wall Shear Rateγ ˙ = (8-34a) w h2w 3 d [log(6Q/h2w)] β = (8-34b) d [log(σw)] σ −∆P h3w Apparent Viscosity η = w = γ˙ w L 4Q(2 + β) NORMAL STRESS DIFFERENCE The normal stress difference N1 can be determined from the exit pressure Pe. dPe N1(γ ˙ w) = Pe + σw (8-45) dσw d(log Pe) N1(γ ˙ w) = Pe 1 + (8-46) d(log σw) These relations were calculated assuming straight parallel streamlines right up to the exit of the die. This assumption is not found to be valid in either experiment or computer simulation. 2 Rheometry SLIT RHEOMETER NORMAL STRESS DIFFERENCE dPe N1(γ ˙ w) = Pe + σw (8-45) dσw d(log Pe) N1(γ ˙ w) = Pe 1 + (8-46) d(log σw) Figure 2: Determination of the Exit Pressure. 3 Rheometry SLIT RHEOMETER NORMAL STRESS DIFFERENCE Figure 3: Comparison of First Normal Stress Difference Values for LDPE from Slit Rheometer Exit Pressure (filled symbols) and Cone&Plate (open symbols). The poor agreement indicates that the more work is needed in order to use exit pressures to measure normal stress differences. -
Guide to Rheological Nomenclature: Measurements in Ceramic Particulate Systems
NfST Nisr National institute of Standards and Technology Technology Administration, U.S. Department of Commerce NIST Special Publication 946 Guide to Rheological Nomenclature: Measurements in Ceramic Particulate Systems Vincent A. Hackley and Chiara F. Ferraris rhe National Institute of Standards and Technology was established in 1988 by Congress to "assist industry in the development of technology . needed to improve product quality, to modernize manufacturing processes, to ensure product reliability . and to facilitate rapid commercialization ... of products based on new scientific discoveries." NIST, originally founded as the National Bureau of Standards in 1901, works to strengthen U.S. industry's competitiveness; advance science and engineering; and improve public health, safety, and the environment. One of the agency's basic functions is to develop, maintain, and retain custody of the national standards of measurement, and provide the means and methods for comparing standards used in science, engineering, manufacturing, commerce, industry, and education with the standards adopted or recognized by the Federal Government. As an agency of the U.S. Commerce Department's Technology Administration, NIST conducts basic and applied research in the physical sciences and engineering, and develops measurement techniques, test methods, standards, and related services. The Institute does generic and precompetitive work on new and advanced technologies. NIST's research facilities are located at Gaithersburg, MD 20899, and at Boulder, CO 80303. -
Navier-Stokes-Equation
Math 613 * Fall 2018 * Victor Matveev Derivation of the Navier-Stokes Equation 1. Relationship between force (stress), stress tensor, and strain: Consider any sub-volume inside the fluid, with variable unit normal n to the surface of this sub-volume. Definition: Force per area at each point along the surface of this sub-volume is called the stress vector T. When fluid is not in motion, T is pointing parallel to the outward normal n, and its magnitude equals pressure p: T = p n. However, if there is shear flow, the two are not parallel to each other, so we need a marix (a tensor), called the stress-tensor , to express the force direction relative to the normal direction, defined as follows: T Tn or Tnkjjk As we will see below, σ is a symmetric matrix, so we can also write Tn or Tnkkjj The difference in directions of T and n is due to the non-diagonal “deviatoric” part of the stress tensor, jk, which makes the force deviate from the normal: jkp jk jk where p is the usual (scalar) pressure From general considerations, it is clear that the only source of such “skew” / ”deviatoric” force in fluid is the shear component of the flow, described by the shear (non-diagonal) part of the “strain rate” tensor e kj: 2 1 jk2ee jk mm jk where euujk j k k j (strain rate tensro) 3 2 Note: the funny construct 2/3 guarantees that the part of proportional to has a zero trace. The two terms above represent the most general (and the only possible) mathematical expression that depends on first-order velocity derivatives and is invariant under coordinate transformations like rotations. -
Rheology of PIM Feedstocks SPECIAL FEATURE
Metal Powder Report Volume 72, Number 1 January/February 2017 metal-powder.net Rheology of PIM feedstocks SPECIAL FEATURE Christian Kukla, Ivica Duretek, Joamin Gonzalez-Gutierrez and Clemens Holzer Introduction constant viscosity is called zero-viscosity h0 (Fig. 1). After a certain > g Powder injection molding (PIM) is a cost effective technique for shear rate ( ˙1), viscosity starts to decrease rapidly as a function of producing complex and precise metal or ceramic components in shear rate, this is known as shear thinning or pseudoplastic behav- mass production [1]. The used raw material, referred as feedstock, ior. For highly filled compounds like PIM feedstocks a yield stress consists of metal or ceramic powder and a polymeric binder can be observed. Thus the viscosity increases dramatically when mainly composed of thermoplastics. The thermoplastic binder decreasing the shear stress and the zero shear viscosity is hard to composition gives plasticity to the feedstock during the molding measure and thus shear thinning is observed even at very low shear g process and holds together the powder grains before sintering. rates. Around a certain higher shear rate ˙2 a second Newtonian > g Most binder systems are made of multi-component systems plateau can be observed and at very high shear rates ( ˙3) the with a range of modifiers which fulfill the above mentioned plateau can change to an increasing viscosity curve due to formation requirements. The flow behavior of the feedstock is the result of of particle agglomerates that can restrict the flow of the binder complex interactions between its constituents. The viscosity of the system. -
Ductile Deformation - Concepts of Finite Strain
327 Ductile deformation - Concepts of finite strain Deformation includes any process that results in a change in shape, size or location of a body. A solid body subjected to external forces tends to move or change its displacement. These displacements can involve four distinct component patterns: - 1) A body is forced to change its position; it undergoes translation. - 2) A body is forced to change its orientation; it undergoes rotation. - 3) A body is forced to change size; it undergoes dilation. - 4) A body is forced to change shape; it undergoes distortion. These movement components are often described in terms of slip or flow. The distinction is scale- dependent, slip describing movement on a discrete plane, whereas flow is a penetrative movement that involves the whole of the rock. The four basic movements may be combined. - During rigid body deformation, rocks are translated and/or rotated but the original size and shape are preserved. - If instead of moving, the body absorbs some or all the forces, it becomes stressed. The forces then cause particle displacement within the body so that the body changes its shape and/or size; it becomes deformed. Deformation describes the complete transformation from the initial to the final geometry and location of a body. Deformation produces discontinuities in brittle rocks. In ductile rocks, deformation is macroscopically continuous, distributed within the mass of the rock. Instead, brittle deformation essentially involves relative movements between undeformed (but displaced) blocks. Finite strain jpb, 2019 328 Strain describes the non-rigid body deformation, i.e. the amount of movement caused by stresses between parts of a body. -
Strain Examples
Lecture 14: Strain Examples GEOS 655 Tectonic Geodesy Jeff Freymueller A Worked Example Θ = e ε + ω dxˆ dxˆ • Consider this case of i ijk ( km km ) j m pure shear deformation, and two vectors dx and ⎡ 0 α 0⎤ 1 ⎢ ⎥ 0 0 dx2. How do they rotate? ε = ⎢α ⎥ • We’ll look at€ vector 1 first, ⎣⎢ 0 0 0⎦⎥ and go through each dx(2) ω = (0,0,0) component of Θ. dx(1) € (1)dx = (1,0,0) = dxˆ 1 (2)dx = (0,1,0) = dxˆ 2 € A Worked Example • First for i = 1 Θ1 = e1 jk (εkm + ωkm )dxˆ j dxˆ m • Rules for e1jk ⎡ 0 α 0⎤ – If j or k =1, e = 0 ⎢ ⎥ 1jk ε = α 0 0 – If j = k =2 or 3, e = 0 ⎢ ⎥ € 1jk ⎢ 0 0 0⎥ – This leaves j=2, k=3 and ⎣ ⎦ j=3, k=2 dx(2) ω = (0,0,0) – Both of these terms will result in zero because dx(1) • j=2,k=3: ε3m = 0 • j=3,k=2: dx3 = 0 € – True for both vectors (1)dx = (1,0,0) = dxˆ 1 (2)dx = (0,1,0) = dxˆ 2 € A Worked Example • Now for i = 2 Θ2 = e2 jk (εkm + ωkm )dxˆ j dxˆ m • Rules for e2jk ⎡ 0 α 0⎤ – If j or k =2, e = 0 ⎢ ⎥ 2jk ε = α 0 0 – If j = k =1 or 3, e = 0 ⎢ ⎥ € 2jk ⎢ 0 0 0⎥ – This leaves j=1, k=3 and ⎣ ⎦ j=3, k=1 dx(2) ω = (0,0,0) – Both of these terms will result in zero because dx(1) • j=1,k=3: ε3m = 0 • j=3,k=1: dx3 = 0 € – True for both vectors (1)dx = (1,0,0) = dxˆ 1 (2)dx = (0,1,0) = dxˆ 2 € A Worked Example • Now for i = 3 Θ3 = e3 jk (εkm + ωkm )dxˆ j dxˆ m • Rules for e 3jk ⎡ 0 α 0⎤ – Only j=1, k=2 and j=2, k=1 ⎢ ⎥ are non-zero -α ε = α 0 0 € ⎢ ⎥ • Vector 1: ⎣⎢ 0 0 0⎦⎥ ( j =1,k = 2) e dx ε dx (2) 312 1 2m m dx ω = (0,0,0) =1⋅1⋅ (α ⋅1+ 0⋅ 0 + 0⋅ 0) = α α ( j = 2,k =1) e321dx2ε1m dxm (1) = −1⋅ 0⋅ (0⋅1+ α ⋅ 0 + 0⋅ 0) = 0 dx • Vector 2: ( j =1,k = 2) e312dx1ε2m dxm € € =1⋅ 0⋅ (α ⋅ 0 + 0⋅ 0 + 0⋅ 0) = 0 (1)dx = (1,0,0) = dxˆ 1 ( j = 2,k =1) e dx ε dx 321 2 1m m (2)dx = (0,1,0) = dxˆ = −1⋅1⋅ (0⋅ 0 + α ⋅1+ 0⋅ 0) = −α 2 € € Rotation of a Line Segment • There is a general expression for the rotation of a line segment. -
Equation of Motion for Viscous Fluids
1 2.25 Equation of Motion for Viscous Fluids Ain A. Sonin Department of Mechanical Engineering Massachusetts Institute of Technology Cambridge, Massachusetts 02139 2001 (8th edition) Contents 1. Surface Stress …………………………………………………………. 2 2. The Stress Tensor ……………………………………………………… 3 3. Symmetry of the Stress Tensor …………………………………………8 4. Equation of Motion in terms of the Stress Tensor ………………………11 5. Stress Tensor for Newtonian Fluids …………………………………… 13 The shear stresses and ordinary viscosity …………………………. 14 The normal stresses ……………………………………………….. 15 General form of the stress tensor; the second viscosity …………… 20 6. The Navier-Stokes Equation …………………………………………… 25 7. Boundary Conditions ………………………………………………….. 26 Appendix A: Viscous Flow Equations in Cylindrical Coordinates ………… 28 ã Ain A. Sonin 2001 2 1 Surface Stress So far we have been dealing with quantities like density and velocity, which at a given instant have specific values at every point in the fluid or other continuously distributed material. The density (rv ,t) is a scalar field in the sense that it has a scalar value at every point, while the velocity v (rv ,t) is a vector field, since it has a direction as well as a magnitude at every point. Fig. 1: A surface element at a point in a continuum. The surface stress is a more complicated type of quantity. The reason for this is that one cannot talk of the stress at a point without first defining the particular surface through v that point on which the stress acts. A small fluid surface element centered at the point r is defined by its area A (the prefix indicates an infinitesimal quantity) and by its outward v v unit normal vector n . -
2 Review of Stress, Linear Strain and Elastic Stress- Strain Relations
2 Review of Stress, Linear Strain and Elastic Stress- Strain Relations 2.1 Introduction In metal forming and machining processes, the work piece is subjected to external forces in order to achieve a certain desired shape. Under the action of these forces, the work piece undergoes displacements and deformation and develops internal forces. A measure of deformation is defined as strain. The intensity of internal forces is called as stress. The displacements, strains and stresses in a deformable body are interlinked. Additionally, they all depend on the geometry and material of the work piece, external forces and supports. Therefore, to estimate the external forces required for achieving the desired shape, one needs to determine the displacements, strains and stresses in the work piece. This involves solving the following set of governing equations : (i) strain-displacement relations, (ii) stress- strain relations and (iii) equations of motion. In this chapter, we develop the governing equations for the case of small deformation of linearly elastic materials. While developing these equations, we disregard the molecular structure of the material and assume the body to be a continuum. This enables us to define the displacements, strains and stresses at every point of the body. We begin our discussion on governing equations with the concept of stress at a point. Then, we carry out the analysis of stress at a point to develop the ideas of stress invariants, principal stresses, maximum shear stress, octahedral stresses and the hydrostatic and deviatoric parts of stress. These ideas will be used in the next chapter to develop the theory of plasticity.